Heterogeneous Uptake of Sulfur Dioxide On Aluminum and

Heterogeneous Uptake of Sulfur Dioxide On Aluminum and Magnesium Oxide Particles ... with Coordinatively Unsaturated Metal Organic Frameworks: M-MOF-7...
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J. Phys. Chem. A 2001, 105, 6109-6120

6109

Heterogeneous Uptake of Sulfur Dioxide On Aluminum and Magnesium Oxide Particles A. L. Goodman, P. Li, C. R. Usher, and V. H. Grassian* Departments of Chemistry and Chemical and Biochemical Engineering, UniVersity of Iowa, Iowa City, Iowa 52246 ReceiVed: December 7, 2000; In Final Form: April 11, 2001

In this study, the heterogeneous uptake of SO2 on R-Al2O3 and MgO particles at 296 K was investigated. Transmission FT-IR experiments reveal that under dry conditions SO2 reacts with R-Al2O3 and MgO to form strongly adsorbed bisulfite, HSO3-(aq), and sulfite, SO32-(aq), on R-Al2O3 and sulfite on MgO. To quantify the uptake of SO2 under dry conditions, heterogeneous uptake coefficients were measured with a Knudsen cell reactor. The Knudsen cell data were modeled to account for gas diffusion in to the underlying layers and surface saturation. The initial uptake coefficient, γo, is calculated using the BET surface area of the powdered samples as diffusion of SO2 into the powder is found to readily occur. Values of γo were determined to be 9.5 ( 0.3 × 10-5 and 2.6 ( 0.2 × 10-4 for SO2 uptake on R-Al2O3 and MgO, respectively, at 296 K under dry conditions at a gas concentration near 1 × 1011 molecules/cm3. Additionally, water uptake on sulfitecoated R-Al2O3 and sulfite-coated MgO particles was investigated with FT-IR spectroscopy. In the presence of adsorbed water, some of the adsorbed sulfite converted to sulfate on MgO but not on R-Al2O3. Atmospheric implications of these studies on SO2 uptake on mineral dust aerosol are discussed.

Introduction Gas-phase nitrogen and sulfur oxides can react with mineral aerosol to form particulate nitrate and sulfate. Recent atmospheric modeling studies have suggested that mineral aerosols have a significant impact on the chemistry of trace tropospheric gases, such as nitrogen and sulfur oxides.1,2 Analysis of aerosol particles offers support of this suggestion as mineral aerosols are often found to be coated with sulfates and nitrates.3-14 As a result, the mechanisms and reaction probability or uptake coefficient of trace tropospheric gases on mineral aerosols have been under investigation.15-24 Reaction of SO2 on mineral aerosols is complicated because the mechanism for SO2 oxidation on mineral particles to form sulfate is uncertain.1 In the troposphere, gas-phase SO2 reacts to produce sulfur trioxide, which is then rapidly converted to sulfuric acid in the presence of water vapor according to reactions 1 and 2.25

SO2 + OH + O2 f SO3 + HO2

(1)

SO3 + H2O f H2SO4

(2)

SO3 in the marine boundary layer is oxidized to sulfate by O3 and H2O2 on sea salt aerosol.26-34 Aqueous-phase oxidation of SO2 in liquid droplets and in clouds is also an important process.35-42 Maahs reports that in aqueous aerosols sulfite and bisulfite may react as follows43

SO32- + O3 f SO42- + O2

(3)

HSO3- + H2O2 f HSO4- + H2O

(4)

and

* To whom correspondence should be addressed.

Atmospheric sulfate particles are known to play a role in the global climate by scattering solar radiation and increasing the number of cloud condensation nuclei.44,45 Sulfate-coated mineral dust particles can change this impact as they participate in the hygroscopic deliquescence and efflorescence cycles.46,47 In this study, the heterogeneous uptake of SO2 on two types of oxide particles, R-Al2O3 and MgO, is investigated in order to gain some insight into the heterogeneous uptake of SO2. R-Al2O3 and MgO are characterized as acidic and basic oxides, respectively, and are used here as models for mineral aerosol found in the troposphere. Transmission FT-IR spectroscopy and UV-vis diffuse reflectance spectroscopy were used to gain some mechanistic insight into SO2 uptake. Knudsen cell experiments were done in order to quantify the rates of SO2 uptake in terms of an initial heterogeneous uptake coefficient, γo. Experimental Section For FT-IR measurements, oxide samples were prepared by either pressing or spraying an oxide/water slurry onto half of a tungsten grid (Buckbee Mears, 100 lines/in. tungsten mesh wire widths of 0.0015′′ and thickness of 0.002′′). The other half of the grid was left blank for gas-phase measurements. The grid half coated with the oxide powder was placed inside the infrared cell. The infrared cell used in this study is modified from the design used in previous studies.18,19 The modified infrared cell consists of a stainless steel cube (2.75′′) with two germanium windows and a sample holder. The inside of the stainless steel cube is coated with Teflon in order to avoid gas decomposition on the walls of the infrared cell. The oxide samples prepared on the tungsten grid are secured inside the infrared cell by Teflon coated sample holder jaws. The infrared cell is connected to a vacuum chamber through a Teflon tube and a glass gas manifold with ports for gas introduction and two absolute pressure transducers (range 0.001 to 10.000 Torr and 0.1 to 1000.0 Torr). The total volume of the system is 1506 ( 3 mL (infrared cube

10.1021/jp004423z CCC: $20.00 © 2001 American Chemical Society Published on Web 06/02/2001

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Goodman et al.

Figure 1. Multisample Knudsen cell apparatus used to measure heterogeneous uptake coefficients.

177 ( 2 mL and a glass gas-manifold 1329 ( 1 mL). The vacuum chamber consists of a two stage pumping system; a turbo-molecular/mechanical pump for pumping down to 10-7 Torr and a mechanical pump for rough pumping down to 10-3 Torr. The infrared cell is mounted on a linear translator inside the FT-IR spectrometer. The translator allows both halves of the grid, the blank side for gas phase measurements and the oxide coated side for surface measurements, to be probed by simply moving the infrared cell through the IR beam path. Infrared spectra were recorded with a single beam Mattson RS-10000 spectrometer equipped with a narrow band MCT detector. Typically 250 scans were collected with an instrument resolution of 4 cm-1 in the spectral range extending from 750 to 4000 cm-1. Heterogeneous uptake coefficients were measured with a Knudsen cell reactor. A Knudsen cell reactor consists of a chamber with an isolated sample compartment and a small orifice through which gas-phase reactant and product species can escape to be detected, usually by mass spectrometry. In a typical Knudsen cell experiment, the sample compartment is covered while the walls of the reactor are passivated and a steady state flow is established. Usually the pressure in the cell is kept low enough such that the mean free path of the molecules within the cell is greater than the cell dimensions so that boundary layer effects and homogeneous gas-phase collisions are minimized and can be neglected. The cell can be used at higher pressures, but to ensure molecular flow the mean free path must be at least a factor of 10 greater than the diameter of the escape aperture.48 In the experiments described herein, an effective escape aperture of 0.0129 cm2, which accounts for the Clausing factor, was used.49 The escape constant, kesc, for this aperture was determined to be 0.080 s-1 for SO2. For the experiments described herein, a Knudsen cell reactor coupled to a UTI, DetecTorr II quadrupole mass spectrometer was used to determine uptake coefficients on powdered samples. Although the Knudsen cell used has been described previously,50

it has recently been modified to allow for the analysis of multiple samples (Figure 1). A stainless steel reducing cross (6-2.75′′) now has four individual sample holders attached to a platform which rests on the bottom (6′′) flange. All exposed interior surfaces are coated with Teflon to provide a chemically inert surface. Four Teflon coated aluminum disks attached to four linear translators serve as covers for each of the powdered samples. The geometric area of each of the four sample holders is 5.07 cm2. Since the volume of the sample holder is much smaller than the total volume of 1750 cm3 (